Process of coating a resin impregnated support sheet with a melamine-formaldehyde composition and resulting product



"treaty i i Wolihsiedler', Darren, and winter M. Thomas,

' "Sp'tingHale; ;Co'nn.-," assignors to American Cyanamid "(2ditiphny, New York;.N. Y'.,'a corporation of Mamefiafnrawia Apiilication1March28, 1952,

SjeriaINo. 279.2 24

Thisfiinventionrel-ates'to aprocess for producing surface lamina'tes and, more" particularly, this invention relates tosurface laminates-prepared by coating a support sheet, impregnated with a thermosettingresin, with a paste=likecsuspension of a plasticized, insolubilized melamineeformaldehyde resin in an aqueous alcohol 1 dispersion medium. The coated sheet isdried and thereafter 'heat-andpressure is applied thereto to; produce the-finishednp'roduct. surfaces-laminates produced in accordance with the proceSsiof the'present,invention.

Gneof the-objects of the-present invention is toprorduceaa-suffacelaminatehavingall of the desirable characteristicsof melamineresin laminate generally. A-furtherr-obiect-ofthepresent invention'is to producea surface laminate having" unusual surface-appearance and',properties' in-which'depth of color and excellent durability is'i combinedfwith improved alcohol resistance and resistan'ce'towstaining. A further object of the'present invention is to produce a surface laminate by coatingan impregnated support sheet with-a plasticized, insolubilized mela e -fo rmaldehyde resin paste, thereafter drying. and

ahd li'glit, durable colo'rs. 'Theselsurface laminates generally are used formakihgtabletops and in this use unmodified melamine resins display excellent heat resistance, resistance to alcohol and other properties: However; ther'einforcing-fibrou's matter, par-.

.the' cellulose sheet which is used in the'convenlaminatedetracts from mar and stain resistance and limitsicolo'r efiects which can be obtained. By the pmcessl or the pre's'entinvention, unusual color effects are inane possible and the other properties desired in a laminate siiiface' are obtained. By modifying melamine comprising a melamine-formaldehyde resin and a plasticiaer' which; can be utilized to'prepare these surface la-minates which have the alcohol resistance of the unmodified" melamine resin laminates while displaying the Still further, this invention relates to the "Uni ed-m 'Q spray-dried. The sprayimproved; mar resistance-anddurability of,the;pl asticized melamine-formaldehyde resincomposition laminates. Generally: speaking th is is accomplished by blendin-g a plasticizer such as an alcohol soluble linear polyamide, polyvinyl formal, polyvinyl-acetal or polyvinyl butyral on heated differential rolls wherein the melamine resin is a water'solubleresin at the outset but isrendered insolubilized by the heat treatment received during. the blending, operation on. the heated differential rolls. Thereafter, this plasticized melamine-formaldehyde resin in an insolubiliz ed-"state. must be dispersedina suitable medium in order. that it can'be utilized'in preparing; surface laminates. This dispersingstep is accomplished by millingthe plasticized. insolub ilized resin in some conventional milling machine such as a ball'millin thepresence of-lth'e medium,.name ly an.alcohol aqueous solution.

The milling. step 'is.'continued until"the plasticized resin I is dispersedin the medium'to a paste-like consistency. The composition is'th'en readyfor use. In preparing a surface laminate, one applies the plasticized, insolubilized melamine formaldehyde composition briefly described hereinabove by coating the same on a support -sheetwhich has-been previously impregnated with a thermosetting-resin and'thesupport =sheet-thus coatedis heated-fora-period of time sufiicient to render the coated sheetdry. Thereafter,- the coated sheet is subjected to home and pressure to produce the surface laminate having improved mar resistance andin'rproved alcohol resistance. e v I In the .prior art efforts haveheen made to' iimprove thedurability of surface laminates by incorporating? fabric or fibrous material" in the surface layer inorder to obtain the necessary strength .to 1 resist stresses ,set up in a cured .coatingnpon. a substrata havingdiiferent thermal expansion} and I porosity properties.

The purpose of the present case is, to produce a .distinct' surface. layer of curedresin having-sufficient strength of itsownwith'outbenefit of any reinforcingifiberin corporatedtherein. The surface resin layers of the .present'invention exists as an intimate and integral part of .the'main structure although they .do form a distinctlayer asmicroscopic crossesectioning clearly demonstrates. The

prior art processeshave made use of the fusible, soluble .resin'sbecause these resins provide a convenient means of combining resin with. .paper. .In polymerizing these resins in situ the stresses and strains referred: to hereinab'o've' often causeddefects vto be produced in the-final laminate;

"In order thatthe present invention may be more com- ,pletely'undei-stood, the following examplesare. set forth in" which all parts are parts by weight I Theseexatnples are'sfe forthlsolely 'for the purpose of illustration and any specific" enumeration of detail'contained therein .should n'o't'be interpreted as va limitation on the case'-ex'cept. as indicated liiith'e appended claims.

RESIN,A I V i g A fusible; solublemelamine resin is prepared by mixing 5l' 2 part's"37% formaldehyde'solution, 386 parts of n'ilamine' 'at' atemperature of '80 F. and adjusted with 'sodiutm Xidefto' a p'IiI' of approximately (glass elej'ctifo e The slurry is .heated' to: reflux," 3.0 to '40 minutes being requiredto raise the temperature/to this isthen checked and adjusted to between At thispoint, the materialis slowlycoole'd whilevisc'osity tests are made; When the reaction syrup reachesa viscosity 'at'25 C. of4550 seconds (Stormer) the syrupf i's adjusted-in 'pHto approximately 9.5 and ing conditions are such as to" produces product-which; the-form of a 5'0%'---so1tds aqueous solution; hasa' viscosity of i2128 'ce'ntipoises'-'at I Patented. Mar. 20, 19,56

RESIN B In order to convert Resin A from a fusible, soluble form to a fusible insoluble form in which its degree of polymerization is suitable for direct molding it was heat treated according to conditions described in U. S. Patent 2,563,630. Resin A, in ground form, is spread on trays and then is oven heated. It is heated at approximately 100 C. for hours and then at 125 C. until a portion slurried with an equal weight of water gave a smooth nonsticky paste, l-3 hours heating at this higher temperature usually, being sufficient. In comparison with Resin A, the product of the foregoing treatment when agitated with an equal weight or an excess of water dissolved to the extent of less than of itsweight.

A resin having substantially the same fusibility and insolubility characteristics is prepared by polymerization on heated differential rolls. With both fast and slow rolls operating at 120 C. and Resin A as the starting material, 33 minutes were sufficient to produce the desired insolubility while retaining fusibility.

Example 1 Parts by weight Resin B- Plasticizer (polyamide) 22 Pigment (titanium dioxide) 90 v Ethyl alcohol 75 Water 225 Mold lubricant 1.1

The resin and pigment were ground and mixed in a ball 'mill. The other ingredients were; added and blended for 16 hours to give a smooth dispersion having a consistency level contact therewith. The coating weight approximated 15 gs. of solids per square foot. The coated sheet was oven dried on a frame for 10 minutes at 90C. The support sheet used in this case was one which had been saturated with a melamine-formaldehyde resin in the form of a syrup and dried. Such asheet is one used in conventional melamine resin laminating practice and there fore the resin is in a fusible state.

Final products were made by superimposing the resin coated sheets on relatively inexpensive core stock and pressing in a laminating press at 250800 p. s. i. and 150 C. for minutes. Suitable core stock for this purpose are paper sheets such as kraft paper sheets which have been saturated with phenolic or other thermosetting resin which is still in a fusible condition. In the pressing or curing operation, the thermosetting resins in the various strata of the assembly areconverted from the fusible to the infusihle state. The phenolic resin core stock may be replaced by Masoniteor resin impregnated compressed wood. These cured articles may be removed from the press While hot but preferably after cooling. A plurality of these products were prepared in which the plasticizer was nylon (an alcohol soluble linear polyamide) used alone or with a secondary plasticizer such as orthocresylglyceryl ether or where the plasticizer was polyvinyl butyral used alone or with a secondary plasticizer such as orthocresylglyceryl ether. These products had excellent the resin and plasticizer were not blended on heated differential rolls until the resin Was rendered substantially completely insolubilized.

Example 2 A surfacing resin is prepared by mixing 25 parts of an alcohol soluble polyamide Nylon FM-lOl and 10 parts monoorthocryesylglyceryl-ether in a Banbury mixer at 155 C. The product in the form of a tough plastic mass is transferred to the differential hot rolls followed by parts of a soluble fusible melamine-formaldehyde resin (Resin A) and one part of zinc stearate. The mix isthen blended with both rolls operating at150 C. for 8 minutes at which point the melamine resin is substantially completely insolubilized, thereafter the plasticized resin is removed from the rolls in the form of a sheet.

This resin sheet is subdivided to granular form and in this state 110 parts are ball milled with 90 parts of titanium dioxide pigment and 300 parts of a mixture of one part of ethyl alcohol to 3 of water. The resin. and vehicle are blended for 16 hours, at the end of which period a smooth coating paste is obtained.

This paste is applied according to the procedure outlined in the above example to obtain surface laminated panels having excellent appearance, color depth, and gloss and superior resistance to abrasion, heat, steam, and particularly reagents such as alcohol, acid and alkali. It should be noted here that the resultant laminated panels produced have all of the desirable attributes with respect to appearance, color, depth, gloss, superior resistance to abrasion heat and steam and additionally displayed no attack whatever when exposed to alcohol. Furthermore, the laminate showed excellent resistance to acids and alkalis. In determining whether a panelhad resistance to alcohol, the latter was maintained in contact with the surface continuously over 16 hours. If the surface has marred in any way, the panel was considered nonresistant.

' Example 3 parts of melamine-formaldehyde resin (ResinA), 15 parts of crystalline polyamide Nylon FM -l0l (Dupont), 5 parts of cresyl glyceryl ether, and one part of zinc stearate were charged to differential rolls heated at 135 C. (fast roll) and 65 C. (slow roll) and blended for 21 minutes, after which the polymerized plasticized resin was removed therefrom in the form of a sheet.

110 parts of the resin obtained by this process were ball milled with parts of titanium dioxide pigment, 75 parts of ethanol and 225 parts of water. After blending this mixture for 16 hours, a coating paste was obtained which yielded cured surfaces having excellent resistance to reagents, particularly alcohol, and durability as revealed by exposure to dry heat and steam, substantially the same as in the case of the product of Example 2.

Example 4 72.5 parts of a melamine-formaldehyde resin (Resin A) 20 parts of polyvinyl butyral, 7.5 parts of cresyl glyceryl ether, and one part of zinc stearate were charged to differential rolls heated at 130 C. (fast. roll) and 65 C. (slow roll) and blended for 21 minutes, and removed therefrom as a sheet. The sheet was micro pulverized and mixed in the proportion of parts with 90 parts of titanium dioxide pigment. The pigmented resinwas made into a paste according to the procedure and with the vehicle of Example 3. Panels having surface properties comparable to Example 2 were obtained.

Good results were obtained by the above technique with the crystalline polyamicles and polyvinyl acetals, including polyvinyl formal, polyvinyl acetal and polyvinyl butyral. Superior results were obtained, however. with the polyamides and polyvinyl butyral; and, it was ascertained that a minimum of 15% of these materials should be used, and preferably 20% to 25% since optimum durability is obtained in this range without diaz'zstaosi minishing the otherd'esirable properties. One" could; I of course, use larger quantities of'the plasticiief such-asap to-40% by'we'ight based on the total weight'ofresin and plasticizer, particularly wher'ethe property ofpost-formability is desired in the cured laminate.

Plasticizers that have been found to give satisfactory results include the crystalline-linear polyamides of the alcohl-or alcohol-water soluble types maximum water content about 25% having softening points below 165 C. at'atmospheric pressure or below approximately 155 .C. under slight pressure such as 50 1bs./sq. in. derived from interpolymerization of a diamine; a dicarboxylic acid and an aminocarboxylic acid or amide forming derivative. A typical polyamide, for example, maybe prepared by reacting 6 parts hexamethylene di ammonium a'dipate and 3.5'parts caprolactam ora corresponding amount of s-arninocaproic acid under polyarnide forming conditions. More than one diamine or dicarboxylic acid may be used but in each polyamide forming compositionthe diarnine ,and dicarboxylic acid must be in substantially equimolecular proportions. Thus,

2' mols of e-caprolactam, 0.5,mol hexamethylene diam- -moniumadipate and 0.5 mol hexamethylene diammonium sebacatewere heated together with a small amount of waterlto 17 0 C. and from 170 C., the temperature was raised to 235,? C. in 4 h0urs where the polyamide was cold;'drawable to a strong film. Its softening point was 130 C., it dissolved readily in alcohol and its intrinsic viscosity was 0.71. By comparison, a polyamide made similarly from 2 mols e-caprolactam and 1 mol hexamethylen'e. diammonium sebacate had a softening point of- 145 C. and an intrinsic viscosity of 0.81. Its alcohol solution, made by warming, tended to gel'zon cooling.

Theyfollowing table presentssome typical polyamideswith their compositions in parts by weight. and properties.

The ethanol or ethanol-water soluble polyamides'jalje the preferred types since they have been found to have the requisite compatibility with melamine forinaldeliyde resin. Their melting or softening points are generally in a suitable range for blending with melamine resin' a'nd even thotigh their softening points at atmospheric pressure may be as high as 165 C., under the shearingpressure of differential rolls their flow temperaturesare-lowered and this permits them to be successfullyblended with melaminle'resin at such temperaturesfas 135-150- C; or

.even lower in some cases. In order to obtain the necessarytoughness and flexibility in the polyamide it is generally necessary to carry their polymerization to a point where their intrinsic viscosity isabout 0:25 or vhigher.

These are p,

produce the resin from E 35 to of same: Polyamides'ofi the preferred type whichare commercially availabie-zinch l'de:those known"as"-Nylon""- FM FIOI L JM-16'377" pioduced-by E.' I. Du PofrtrdeFNeniours": They have softening' points between and C: and a'realcoh'ohor-alcohobwater soluble. PM -100 is ma'rkeidby an in-trinsierviscosityof 1.3-1. Polyamides of the-*high: melting type (softening point C. or higher)suchasthatderived-from hezcamethylene diammonium-adipat'e are'ofno direct-utility inthe practice of thisinvention. p 7 Poly-vinyl a'eetals includingwthose; more specifically i na as po y ny o malnpoly ny ac n Po ythe e s of hi e upla ede i ed:frq p y y a e yt complet ana a h r l s of ace 10 hYdt Y u ld:brr ac aw t ahal h d whereby the hydronyl groups are" converted to the acetal linkage. For satisfactory perf ance; certain compositional features are pr e hydrokyl groups are as r 'bl i f a wit atib is. wi hthsm am n ra dehyderesin. Gein era'llyi 25%; of h-y 0 1 calculated as polyvinyl arcane Should b p resent a min uin qu n ity eri aeetae'stieii ss o expressedlas'ipolyvinyl olyv t 'v henna in uie material; and the pretense liibncant s z nc stearate.

A product pos'ssis'i'rig siiperior to that, abrasion,- reagents; I l e atobtained byemploying a hot of polymerization wherein aplas'ticiz'er, and rr'eq'u t "One prti'c "s bieniis thef-pla sticizer blend is then rolled and sheeted with the 'melamine resin In this region of polymerization they exhibit a crystalline X ray'pattern. Suitable starting materials for the preparation of the polyamides include such diarnines as ethyl by weight of the starting composition or more generally point of the- ;in ary"p1asiiizer" is the "fang e'of normal fw lie're -they-are mixedan M H I k peratureadjustment." In both of thesie f processes, he

i and preferably a rolling*and molding lubricant; "such as zinc mar ne. The otlierpiocess A be considered 'a v v n V n components-inn dry-blendedstate are charged ttylreated secondary "plasticiz'e'r is em eyed-mama the softening rolling temperatures 'for"t hesak "of compat'ibililty; In cases wherein the primary plasticizen has-ya softening .point within the range of the njornial rolling temperatures,

the secondary plasticizers maybe omitted; Roir'temper'amm and rollingt-ime arseentr'onen; in'the'se cases to eifect 'afairly-stitf flow. i

persi'on medium, one can-make asssr ne vous-tanner soluble monohydric alcohols and, more particularly, the lower aliphatic alcohols having between 1 and 4 carbon atoms such as methanol, ethanol, propanol, isopropanol, secondary butanol, isobutanol and tertiary butanol. The amount of alcohol present in the aqueous solution should be held within the range of about to about 50% by weight based on the total weight of the aqueous alcohol solution and preferably between and 40% by weight.

The amount of plasticized resin dispersed in the aqueous alcohol medium should be between about 20% and 40% by weight based on the total weight of the plasticized resin and the dispersion medium; preferably between and by weight of theplasticized resin based on the total weight of said resin and dispersion medium.

The pigmented resin coating dispersions appear to be more stable than unpigmented dispersions. Apparently, the pigment particles seem to aid in preventing resin from agglomerating. The pigmented resin coating dispersions, fromwhich a water layer has separated, may be restored to its original condition by stirring or shaking, and in this sense are considered indefinitely stable.

Other pigments than those specifically mentioned in the example may be used including the mineral pigments such as zinc sulfide, lithopone, cobalt blue, chrome oxide, selenium pigments, lake colors or dyestuffs. The pH of the pastes or dispersions may be adjusted by the addition of acid or alkaline reagents or buffers in order to linear polyamide or the polyvinyl acetal plasticizers may.

be found in copending application, Serial No. 684,782,

filed July 19, 19.46, now Patent No. 2,546,841, and Serial No. 684,781,'filed July 19, 1946, now abandoned. Certain copolymei's are also of value as plasticizers. These include copolymers derived from monomers such as acrylonitrile and ethylacrylate and N-substituted acrylamides as set forth in U. S. Patent No. 2,582,303, to Wohnsiedler and Kropa. Copolymers of acrylonitrile and vinyl acetate and copolymers of ethyl acrylate and 2,4- dimethyl styrene.

The melamine-formaldehyde resins used in the practice of the process of the present invention are of the nonalkylated variety, namely those which do not have, as an essential reactant, a compound containing an alcoholic hydroxy group such as methanol, butanol and the like. The essential reactants of the resin are melamine and formaldehyde and should be present in mol ratios varying between 1:1.5 and 1:6, but preferably 1:2 to 1:3, respectively. U

In the drying step wherein the impregnated sheet, coated with the resinous paste, is dried prior to the application of heat and pressure to produce the laminate, one

can accomplish this drying step by subjecting the coated sheet totemperatures between about C. and 90 C.

Quite obviously, one could use temperatures below 60 C. or above 90 C. but in the former instance, a much '750 and 1500 p. s. i.

The preferred pressurev range should be between about The amount of time required in this particular step will vary substantially with the temperature from about 10-15 minutes at the higher temperatures to about 1 or more hours at the lower temperature.

In the blending step, wherein the water soluble melamine resin is combined with the plasticizer on the heated ditferential rolls, it has been indicated hereinabove thatit isdesired that the blending operation be continued until the resin is substantially insolubilized. By this, it is intended that the resin shall be polymerized sufiiciently so that it is soluble in water only to the extent of about 2%-15% and preferably closer to the lower limit. This is accomplished while still retaining the resin in a condition in which it exhibits fusibility and flow under the final molding conditions.

The plasticizcd surfacing compositions in the form of their aqueous-alcohol dispersions may be applied to other substrata of a character similar to the thermosetting resin impregnated sheet which serves as the carrier sheet for the preparation of laminates. For example, they may be sprayed on partially cured molded objects derived from phenolic, urea, melamine or other thermosetting resin molding compositions. Thereafter, the coating may be dried and the object given a final heat treatment in the original mold cavity to unite the surface plastic with the base plastic and to cure the assembly as a whole. Thereby, a decorative surface or one possessing unusual durability and resistance to staining may be applied.

. A plurality of panels were prepared according to the process of Example 1 and of Example 2 with varying amounts of primaryplasticizer and varying amounts of primary plasticizer plus secondary plasticizer and the panels were subjected to the alcohol test. The results are set forth hereinbelow:

ATTACK BY ALCOHOL Procedure of Example 1 Procedure of Example 2 Plastlclzer Plastlclzer Plastlclzer, Percent g k gfg Plasticizer, Percent and Resin 0t Surfacing Com- Treated of Surfacing Com- Reacted position position on Hot Melamine Rolls Resin 20Nylon severe. 25Nylon 20Nylon-. o. lO-Crcsylglycerlne none. 20Ny1on- Do. ether. 15Nylon Do. 15Nylon 5-Oresyl glycerlne Do. 5-Cresyl glycerlne Do. zo i l 1 b D zo i v b 1 p0 yv ny u- 0. utym tyral. 7.5Benzamlde 10P. V. butyraL-.. 5-('i1resyl glycerlne Do.

er. 15-1. V. butyral 15-1. V. butyral--. 5-Cresyl glycerine Do. 5Cresyl glycerine Do.

ether. ether.

We claim:

1. A process for producing a surface laminate comprising coating a support sheet, impregnated with a thermosetting resin, with a composition comprising a pastelike suspension of a plasticized, insolubilized, fusible melamine-formaldehyde resin in an equeous alcohol medium, heating said coated sheet to dryness and applying to said dried, coated sheet heat and pressure until said composition is rendered infusible, wherein the plasticized resin suspension is prepared by blending a soluble melamine-formaldehyde resin and a plasticizer on heated differential rolls until the melamine-formaldehyde resin is rendered insolubilized but fusible, thereafter milling said plasticized resin with an aqueous solution of a volafile, water-soluble monohydric alcohol having between 1 and 4- carbon atoms'until a paste-like suspension is produced wherein said plasticizer is a member selected from the group consisting of (a) an alcohol or alcohol-Water soluble linear polyamide having a softening point below about 165 C., (b) polyvinyl formal, polyvinyl acetal and polyvinyl butyral, wherein said acetals have a hydroxyl content, expressed as polyvinyl alcohol, between about and by weight based on the total weight of said acetal, wherein the proportions of resin to plasticizer are within the range of 85:15 to 60:40 parts by weight, respectively, wherein the weight ratio of the plasticized resin to the water-alcohol dispersion medium is within therange of about :60 to 20:80 parts by weight, respectively, and wherein the weight ratio of the water to alcohol is about 90:10 to about :50, respectively.

2. A process for producing a surface laminate comprising coating a support sheet, impregnated with a thermosetting resin, with a composition comprising a pastelike suspension of a plasticized, insolubilized, fusible melamine-formaldehyde resin in an aqueous alcohol medium, heating said coated sheet to dryness and applying to said dried, coated sheet heat and pressure until said composition is rendered infusible, wherein the plasticized resin suspension is prepared by blending a soluble melamine-formaldehyde resin and a plasticizer on heated differential rolls until the melamine-formaldehyde resin is rendered insolubilized, thereafter milling said plasticized resin with an aqueous solution of volatile water soluble monohydric alcohol having between 1 and 4 carbon atoms until a paste-like suspension is produced wherein said plasticizer is a member selected from the group consisting of polyvinyl acetal and polyvinyl butyral, wherein said acetals have a hydroxyl content, expressed as polyvinyl alcohol between about 10% and 20% by weight, based on the total weight of polyvinyl acetal, wherein the proportions of resin to plasticizer are within the range of 80:20 to :30 parts by weight, respectively, wherein the weight ratio of the plasticized resin to the water-alcohol dispersion medium is within the range of about 35:65 to 25:75 parts by weight, respectively, and wherein the'weight ratio of the water to alcohol is about :20 to 60:40, respectively.

3. The process according to claim 1 in which the plastieizer is an alcohol soluble linear polyamide having a softening point below about C.

4. The process according to claim 1 in which the plasticizer is a polyvinyl butyral having a hydroxyl content expressed as polyvinyl alcohol between about 16% and 22% by weight.

5 A surface laminate produced according to the process of claim 1.

6. A surface laminate produced according to the process of claim 3.

No references cited. 

1. A PROCESS FOR PRODUCING A SURFACE LAMINATE COMPRISING COATING A SUPPORT SHEET, IMPREGNATED WITH A THERMOSETTING RESIN, WITH A COMPOSITION COMPRISING A PASTELIKE SUSPENSION OF A PLASTICIZED, INSOLUBILIZED, FUSIBLE MELAMINE-FORMALDEHYDE RESIN IN AN EQUEOUS ALCOHOL MEDIUM, HEATING SAID COATED SHEET TO DRYNESS AND APPLYING TO SAID DRIED, COATED SHEET HEAT AND PRESSURE UNTIL SAID COMPOSITION IS RENDERED INFUSIBLE, WHEREIN THE PLASTICIZED RESIN SUSPENSION IS PREPARED BY BLENDING A SOLUBLE MELAMINE-FORMALDEHYDE RESIN AND A PLASTICIZER ON HEATED DIFFERENTIAL ROLLS UNTIL THE MELAMINE-FORMALDEHYDE RESIN IS RENDERED INSOLUBILIZED BUT FUSIBLE, THEREAFTER MILLING SAID PLASTICIZED RESIN WITH AN AQUEOUS SOLUTION OF A VOLATILE WATER-SOLUBLE MONOHYDRIC ALCOHOL HAVING BETWEEN 1 AND 4 CARBON ATOMS UNTIL A PASTE-LIKE SUSPENSION IS PRODUCED WHEREIN SAID PLASTICIZER IS A MEMBER SELECTED FROM THE GROUP CONSISTING OF (A) AN ALCOHOL OR-WATER SOLUBLE LINEAR POLYAMIDE HAVING A SOFTENING POINT BELOW ABOUT 165*C., (B) POLYVINYL FORMAL, POLYVINYL ACETAL AND POLYVINYL BUTYRAL, WHEREIN SAID ACETALS HAVE A HYDROXYL CONTENT, EXPRESSED AS POLYVINYL ALCOHOL, BETWEEN ABOUT 10% AND 25% BY WEIGHT BASED ON THE TOTAL WEIGHT OF SAID ACETAL, WHEREIN THE PROPORTIONS OF RESIN TO PLASTICIZER ARE WITHIN THE RANGE OF 85:15 TO 60:40 PARTS BY WEIGHT, RESPECTIVELY, WHEREIN THE WEIGHT RATIO OF THE PLASTICZED RESIN TO THE WATER-ALCOHOL DISPERSION MEDIUM IS WITHIN THE RANGE OF ABOUT 40:60 TO 20:80 PARTS BY WEIGHT, RESPECTIVELY, AND WHEREIN THE WEIGHT RATIO OF THE WATER TO ALCOHOL IS ABOUT 90:10 TO ABOUT 50:50, RESPECTIVELY. 